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Steam Enhanced Recovery of BTEX and chlorinated hydrocarbon contaminated groundwater

Data provider

Budapest University of Technology and Economics, Department of Applied Biotechnology and Food Science, Environmental Microbiology and Biotechnology Group

Organisation/Data provider's nameBudapest University of Technology and Economics, Department of Applied Biotechnology and Food Science, Environmental Microbiology and Biotechnology Group
Name of contact
Dr. Molnár Mónika, Dr. Feigl Viktória
Contact details
Telephone/fax
+36-1-4632347
Compulsory sheet of the technology
Technology Hungarian nameSteam Enhanced Recovery of BTEX and chlorinated hydrocarbon contaminated groundwater
Technology name
Gőz injektálás BTEX-szel és halogénezett alifás szénhidrogénnel szennyezett talajvíz remediálására
Country of origin
Egyesült Királyság
Stage of development
developed, proven by demonstration
Standard number
Hungarian version in Nr. 651
Financing of the project
Application sphere
Contaminant group|Contaminant typically treated
  • Halogenated aliphatic organic compounds
  • trichloroethane
Other contaminants
other chlorinated metabolites or derivatives
Contaminant group|Contaminant typically treated
  • Halogenated aliphatic organic compounds
  • tetrachloroethylene
Other contaminants
other chlorinated contaminants
Contaminant group|Contaminant typically treated
  • Halogenated aliphatic organic compounds
  • vinyl chloride
Contaminant group|Contaminant typically treated
  • Halogenated aliphatic organic compounds
  • 1,1-dichloroethane
Contaminant group|Contaminant typically treated
  • Benzene and alkyl benzenes (BTEX)
  • m-xylene
Description of environmental risk
Maximum initial value
27 µg/l
Contaminant group|Contaminant typically treated
  • Halogenated aliphatic organic compounds
  • 1,1,1-trichloroethane
Information on the technology
Environmental element/phase the method may be applied to
Saturated soil
Subsurface water
Technology type
combined
Basis of the technology
Ecological
Technology description

The technology involves the injection of high pressure steam into an aquifer to thermally enhance conditions so that remediation can be completed at an accelerated rate. Once optimum temperatures have been achieved a high vacuum steam ejector system is used to extract vapours and groundwater. All of the recovered vapour and liquors are cooled in a heat exchange condenser prior to treatment through GAC filters.

Description of the novelty of the technology

The innovative combination of a DPVE system with a system of injecting steam enabled the in-situ treatment of a Xylene impacted clay horizon (located between two permeable horizons) situated above the identified groundwater table. The enhanced system facilitated the delivered steam at high pressure and temperature into the gravel horizon underlying the identified Xylene impacted silt/clay and removed the requirement for excavation.

Technology classification
Remediation technology type
  • thermal
  • soil heating with vapour
Other remediation technology
vacuum extraction of in situ heated groundwater
Remediation technology from contaminant point of view
mobilisation
Remediation technology from execution point of view
in situ
Technology-monitoring
Technological parameters
Water flux
Contaminant amount
Temperature
Monitored environmental element
Saturated soil
Subsurface water
Costs of the technology
Capital costs
40.000 - 200.000 Euro
Specific operation costs
no estimation
Specific energy costs
no estimation
Specific material costs
no estimation
Specific labour costs
no estimation
SWOT (evalaution based on scores)
Costs
3-medium
Time requirement
4-low
Space requirement
3-medium
Workload requirement
3-medium
Equipment, apparata requirement
4-low
Qualified labour
3-medium
Environmental risk and workplace risks
3-medium
Ability to meet the target value
4-high
Environmental efficiency
4-high
Cost efficiency
4-good
Generation of any recyclable byproduct
yes
Generation of any byproduct to be treated
yes
Automation/remote control
yes
Feasibility
4-good
Availability
3-average
Well known
2-weak
SWOT (evaluation in words)
Strengths

The physical flushing action of injected steam and hot condensates; Increasing temperatures to change contaminant physical/chemical properties to increase mobility e.g reducing viscosity, capillary/interfacial forces and contaminant density, increasing volatility and desorption rates; Increasing temperatures to affect a change in contaminant partitioning equilibriums, so that a greater proportion of contaminants exist within the dissolved /vapour phases.
Optimising subsurface temperatures for biodegradation.

A vákuum okozta nyomáscsökkenés és csökkenő koncentrációgradiens a talajgáz/gőz talajból kifelé áramlását nagyban meggyorsítja a spontán diffúzióhoz képes. A másik fontos jellemzője, hogy a gőzformájú szennyezőanyag kontroll alá kerül, a kiszívott talajgázzal együtt.

Weaknesses

Key risks, in relation to health and safety of personnel, focus on the use of pressurised steam. All staff were appropriately trained and operated to robust, comprehensive, health and safety method statements. Staff expertise was essential to the safe operation of the system.

Possibilities

Mobile steam-production unit and recovery system, highly flexible system, depending of the needs of the site and contaminants.

Threats

The effect of heating on soil microflora. The workers risk due to high pressure steam.

Completed applications
Site name
West Drayton
Location of the application, country
Nagy- Britannia
Location of the application, town
London
Application stages
Demonstration
Summary of the charasteristic parameters of application

Heating Phase: steam was injected until target temperatures of 600C-900C were reached in the substrata. Maintenance Phase: upon achievement of optimum temperatures, a dual pump high vacuum extraction system was used to extract vapours and groundwater. During the maintenance phase steam was periodically injected to maintain temperatures. Air sparging was also undertaken, encouraging in-situ hydrous pyrolysis oxidation of contaminants. Oxygen introduced into a heated subsurface acts, as a powerful oxidiser, cost effectively treating contamination. Recovered vapours and liquors were cooled using a heat-exchanging condenser prior to treatment through Granular Activated Carbon (GAC) filters. Cooling/Polishing Phase: Post heating, subsurface temperatures remain elevated (25 0C and 50 0C). Oxygen essential for biodegradation was introduced by sparging air into the saturated zone and through drawing air into the unsaturated zone under vacuum.

Publications, references
Pictures
Properties of the datasheet
Datasheet id (original)
746
Creator
Meggyes Tamas
Status
Verified
Adatlap típusaSoil remediation technology
Létrehozás
Módosítás